The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Jul. 16, 2024

Filed:

Oct. 23, 2019
Applicant:

Sasol South Africa Limited, Sandton, ZA;

Inventors:

Jean Louis Gauché, Potchefstroom, ZA;

Cornelia Pienaar, Vanderbijlpark, ZA;

Jurie Christiaan Wessels Swart, Johannesburg, ZA;

Jan Mattheus Botha, Sasolburg, ZA;

Denzil James Moodley, Vanderbijlpark, ZA;

Jana Heloise Potgieter, Sasolburg, ZA;

Jolandie Zonja Davel, Sasolburg, ZA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 23/89 (2006.01); B01J 8/24 (2006.01); B01J 21/08 (2006.01); B01J 23/00 (2006.01); B01J 35/64 (2024.01); B01J 37/04 (2006.01); B01J 37/08 (2006.01); B01J 37/18 (2006.01); C10G 2/00 (2006.01);
U.S. Cl.
CPC ...
B01J 23/8986 (2013.01); B01J 8/24 (2013.01); B01J 21/08 (2013.01); B01J 23/002 (2013.01); B01J 35/643 (2024.01); B01J 35/647 (2024.01); B01J 37/04 (2013.01); B01J 37/082 (2013.01); B01J 37/18 (2013.01); C10G 2/332 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4018 (2013.01); C10G 2300/70 (2013.01);
Abstract

The invention provides a process for preparing a cobalt-containing catalyst precursor. The process includes calcining a loaded catalyst support comprising a silica (SiO) catalyst support supporting cobalt nitrate to convert the cobalt nitrate into cobalt oxide. The calcination includes heating the loaded catalyst support at a high heating rate, which does not fall below 10° C./minute, during at least a temperature range A. The temperature range A is from the lowest temperature at which calcination of the loaded catalyst support begins to 165° C. Gas flow is effected over the loaded catalyst support during at least the temperature range A. The catalyst precursor is reduced to obtain a Fischer-Tropsch catalyst.


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